Heat exchange systems

Abstract: A cryogenic heat exchange system with particular application to a freeze dryer (1) comprising a heat exchanger (12) having at least one pass (14) for receiving a cryogenic heat exchange fluid; a reversing circuit (16) connected to the at least one pass having an inlet (18) for receiving the cryogenic heat exchange fluid, means for introducing the cryogenic heat transfer fluid into the at least one pass (14) and for reversing flow direction of the cryogenic heat transfer fluid so that the cryogenic heat exchange fluid flows through the at least one pass in one flow direction and then in an opposite flow direction, and an outlet (20) for receiving a portion of the cryogenic heat transfer fluid from the at least one pass (14) after having passed therethrough as spent cryogenic heat exchange fluid; recirculation means connected to the outlet (20) of the reversing circuit (16) for receiving the spent cryogenic heat transfer fluid and having a mixing chamber (40) for mixing the spent cryogenic heat transfer fluid with a cryogen, to form the cryogenic heat exchange fluid and thereby to increase the enthalpy of the cryogenic heat transfer fluid over that of the cryogen, a mixing chamber outlet (38) in communication with the inlet (18) to the reversing circuit (16) for introducing the cryogenic heat transfer fluid into the reversing circuit, and means for circulating the cryogenic heat transfer fluid to the reversing circuit, through the at least one pass and back to the mixing chamber (40) as the spent cryogenic heat exchange fluid; and vent means (30) for venting a remaining portion of the cryogenic heat transfer fluid after having passed through the at least one pass (14) of the at least one heat exchanger (12).

Description: This invention relates to a cryogenic heat exchange system in which a cryogenic heat transfer fluid is circulated through one or more passes of the heat exchanger in order to cool a heat load. Additionally, the present invention relates to a freeze dryer employing the cryogenic heat exchange system wherein the cryogenic heat transfer fluid is circulated through a condenser used in condensing sublimated water vapour (see for example EP 0 301 117 A1). Cryogenic heat exchangers have the advantage that they do not use environmentally damaging refrigerants, but instead use a cryogenic heat transfer fluid such as a liquefied atmospheric gas. Additionally, such cryogenic heat exchangers provide much greater flexibility in the amount of cooling provided and can reach colder temperatures than heat exchangers utilizing conventional refrigerants. It has been found, however, that it is difficult to build such a heat exchanger in a compact fashion because as the cryogenic heat transfer fluid enters the heat exchanger, more ice will build up on the side of the heat exchanger at which the cryogenic heat transfer fluid enters the heat exchanger. The section of the heat exchanger at which the ice has built up will be relatively ineffective as compared to the remainder of the heat exchanger. The ice itself may be unacceptable in come cases, such as in chilling liquids, or may block the heat exchanger. Still another problem is that there is very little control over the temperature of the heat exchanger. Assuming, liquid nitrogen were used as the cryogenic heat transfer fluid, the inlet to the heat exchanger would cool to temperatures of about 77°K. Such cooling would damage certain types of food products and in any event would be inefficient when the article to be cooled were only required to be cooled to about the freezing point of water. The present invention is concerned with the provision of a cryogenic heat exchange system in which ice build-up on a heat exchanger employed in the cryogenic heat exchange system is more uniform (and possibly prevented altogether) as compared with that of known heat exchangers which employ a cryogenic heat exchange fluid. Moreover, the invention can generally provide a cryogenic heat exchange system in which the temperature at which heat transfer takes place can be controlled. In accordance with the invention, there is provided a cryogenic heat exchange system comprising a cryogenic heat exchange system comprising: a heat exchanger having at least one pass for receiving a cryogenic heat exchange fluid; a reversing circuit connected to the at least one pass having an inlet for receiving the cryogenic heat exchange fluid, means for introducing the cryogenic heat transfer fluid into the at least one pass and for reversing flow direction of the cryogenic heat transfer fluid so that the cryogenic heat exchange fluid flows through the at least one pass in one flow direction and then in an opposite flow direction, and an outlet for receiving a portion of the cryogenic heat transfer fluid from the at least one pass after having passed therethrough as spent cryogenic heat exchange fluid; recirculation means connected to the outlet of the reversing circuit for receiving the spent cryogenic heat transfer fluid and having a mixing chamber for mixing the spent cryogenic heat transfer fluid with a cryogen, to form the cryogenic heat exchange fluid and thereby to increase the enthalpy of the cryogenic heat transfer fluid over that of the cryogen, a mixing chamber outlet in communication with the inlet to the reversing circuit for introducing the cryogenic heat transfer fluid into the reversing circuit, and means for circulating the cryogenic heat transfer fluid to the reversing circuit, through the at least one pass and back to the mixing chamber as the spent cryogenic heat exchange fluid; and vent means for venting a remaining portion of the cryogenic heat transfer fluid after having passed through the at least one pass of the at least one heat exchanger. The term "cryogen" used herein and in the claims means a substance existing as a vapour or liquid or a solid at temperatures well below those normally found in ambient, atmospheric conditions. Examples of cryogens are liquefied atmospheric gases, for instance, nitrogen, oxygen, argon, carbon dioxide, etc. The reversing of the flow direction of the cryogenic heat transfer fluid will cause ice to accumulate in uniform amounts on at least the ends of the heat exchanger. At intermediate points, between the ends of the heat exchanger, more ice might build up than on the ends of the heat exchanger. In order to minimize ice build up between the ends of the heat exchanger, the enthalpy of the incoming cryogenic heat transfer fluid is increased by recirculating a portion of the spent cryogenic heat transfer fluid and mixing it with incoming cryogenic liquid to raise the average temperature at which the heat transfer takes place. The reversing flow coupled with the enthalpy boost can in appropriate applications of the present invention be used as a self-defrost feature where ice build-up in any amount is unacceptable. It is to be noted here that the discussion of the heat exchanger with respect to "ice build-up" or "frost" is not meant to limit the field of use of the present invention to instances in which water freezes. The ice or frost in other applications, for instance, food chilling or freezing, could be carbon dioxide as well as other ice or frost forming substances connected with the particular application of the present invention. In preferred embodiments, the heat exchanger has a reversing circuit which comprises a heat exchanger according to Claim 1 in which the reversing circuit comprises: a pair of first and second valves connecting the at least one pass between the inlet and outlet of the recirculation means such that when the first and second valves are set in an open position, the cryogenic heat transfer fluid flows through the at least one pass in the one flow direction; and a pair of third and fourth valves also connecting the at least one pass between the inlet and outlet of the recirculation means such that when the first and second valves are set in an closed position and the third and fourth valves are set in an open position, the cryogenic heat transfer fluid flows through the at least one pass in the opposite flow direction. The recirculation means preferably comprises a venturi-type device having a high pressure inlet for receiving the cryogenic liquid, a low pressure inlet for connection to the outlet of the reversing circuit for drawing the spent cryogenic heat transfer fluid, a low pressure region serving as the mixing chamber and in communication with the high and low pressure inlets, and a high pressure outlet, the high pressure outlet serving as the mixing chamber outlet and connected to the inlet of the reversing circuit for discharging the cryogenic heat transfer fluid into the reversing circuit. The heat exchange system preferably also comprises a recirculation heat exchanger having a first pass connected to the high pressure inlet of the ejector and a second pass communicating between the outlet of the reversing circuit and the low pressure inlet of the ejector for exchanging heat between the cryogen and the spent cryogenic heat transfer fluid prior to the ejector to increase the enthalpy of the ejector. In another aspect, the present invention provides a freeze dryer comprising: a freezing chamber for subjecting substances to a freeze drying process in which moisture contained within the substances is frozen and sublimated into a vapour; a condenser in communication with the freezing chamber for freezing the vapour and for accumulating the vapour as ice, the condenser having at least one pass for receiving a cryogenic heat transfer fluid for freezing the vapour; a reversing circuit connected to the condenser and having an inlet for receiving the cryogenic heat exchange fluid, means for introducing the cryogenic heat transfer fluid into the at least one pass of the condenser and for reversing flow direction of the cryogenic heat transfer fluid so that the cryogenic heat transfer fluid flows in one flow direction and then in an opposite flow direction, thereby to promote a uniform accumulation of the ice on the condenser, and an outlet for receiving a portion of the cryogenic heat transfer fluid from the condenser as spent cryogenic heat exchange fluid; recirculation means connected to the outlet of the reversing circuit for receiving the spent cryogenic heat transfer fluid and having a mixing chamber for mixing the spent cryogenic heat transfer fluid with a cryogen to form the cryogenic heat transfer fluid and thereby to increase the enthalpy of the cryogenic heat transfer fluid over that of the cryogen, a mixing chamber outlet in communication with the inlet to the reversing circuit for introducing the cryogenic heat transfer fluid into the reversing circuit, and means for circulating the cryogenic heat transfer fluid to the reversing circuit, through the at least one pass of the condenser, and back to the mixing chamber as the spent cryogenic heat exchange fluid; and vent means for venting a remaining portion of the cryogenic heat transfer fluid after having passed through the at least one pass of the condenser. For a better understanding of the invention, reference will now be made, by way of exemplification only, to the accompanying drawing showing in schematic form a cryogenic heat exchange system of the invention used within a condensing section of a freeze dryer also in accordance with the invention. With reference to the figure, a freeze dryer 1 is illustrated as employing a freeze drying chamber 10 within which substances are subjected to a freeze drying process and a condenser 12 which forms part of a cryogenic heat transfer system. In the freeze drying process, substances are placed within a freeze drying chamber 10, normally on shelves, and the substances are frozen on the shelves by circulating a refrigerant through passages provided within the shelves. Thereafter, the pressure within the freeze dryer is sufficiently reduced until the frozen moisture contained within the substances sublimates into a vapour. The vapour is drawn into a condenser 12 on which it is frozen. The condenser 12 is provided with one pass 14 through which a cryogenic heat transfer fluid passes. The condenser 12 (or any other heat exchanger to be utilized in connection with the invention) could incorporate more than one pass. In the freeze dryer 1, the cryogenic heat transfer fluid is nitrogen vapour. The nitrogen vapour is introduced into the condenser 12 through the use of a reversing circuit 16 of the cryogenic heat transfer system. Reversing circuit 16 has an inlet 18 and an outlet 20. A tree of first, second, third and forth solenoid operated valves 22, 24, 26 and 28 are provided. When first and second valves 22 and 24 are open, nitrogen vapour flows into the inlet 18, through the first valve 22, through the pass 14, back through the second valve 24 and out of outlet 20. When the first and second valves 22 and 24 are closed and the third and fourth valves 26 and 28 are open, nitrogen vapour flows through the inlet 18, the third valve 26, the pass 14 of the condenser 12 in the opposite flow direction, back through the fourth valve 28, and then out of the outlet 20. It is to be noted that alternative valving arrangements could be used such as three-way valves. A portion of the nitrogen vapour is recirculated while a remaining portion of the nitrogen vapour is vented preferably through an adjustable pressure relief valve 30. The pressure relief valve 30 is adjusted to maintain an elevated pressure within the cryogenic heat exchange system and thereby to minimise pressure drop and flow velocity within the heat exchanger. The maintenance of pressure also allows exhaust nitrogen vapour to be delivered at a sufficiently high delivery pressure so as to be used elsewhere in an installation either utilizing either the freeze dryer 1 or a cryogenic heat exchange system in accordance with the present invention. Venting could also be controlled by other valving such as a regulating valve or a pressure switch/valve combination. The cryogenic heat exchange system is also provided with an ejector 32 to effect circulation of the nitrogen vapour acting as the cryogenic heat transfer fluid. The ejector 32 has a high pressure inlet 34 and a low pressure inlet 36. The ejector 32 is also provided with a diffuser section 37 for pressure recovery. The diffuser section 37 terminates in an outlet 38 for discharging the cryogenic heat transfer fluid. The recirculated portion of the cryogenic fluid is drawn into the low pressure inlet 36 of the ejector 32 by a low pressure region produced within the ejector 32. Although not illustrated, such a low pressure region is produced by a venturi effect due to the flow of incoming cryogen entering the ejector 32 through the high pressure inlet 34. Other venturi-type devices, having high and low pressure inlets, a low pressure region for mixing, and a high pressure outlet, not necessarily termed "ejectors" could serve the same purpose as ejector 32. In the illustrated embodiment, the incoming cryogen is liquid nitrogen supplied at a gauge pressure of about 1035 kilopascals and a temperature of about minus 185° C. The high and low pressure inlets 34 and 36 and the diffuser section 37 all communicate with a low pressure region, designated by reference number 40. The low pressure region 40 serves as a mixing chamber in which the incoming cryogen, which may in fact be in a vapour form, mixes within the portion of the spent cryogenic heat transfer fluid, that is nitrogen vapour after having passed through condenser 12 to form the cryogenic heat transfer fluid. The pressure of the cryogenic heat transfer fluid is to some extent recovered in the diffuser section 37 and is then discharged to the high pressure outlet 38 which serves as an outlet of the mixing chamber. The high pressure outlet 38 is connected to the inlet 18 of the reversing circuit 16. As can be appreciated, such mixing also increases the enthalpy of the cryogenic heat transfer fluid to be circulated over the enthalpy of the entering liquid nitrogen. The increase in enthalpy coupled with flow reversal promotes uniform ice formation on the condenser 12. If appropriate, the same principle could be used to provide a cryogenic heat exchanger with a self-defrost function. The ejector 32 is preferred because it has no moving parts and the heat transfer is efficiently conducted between the incoming cryogen and the cryogenic heat transfer fluid. It is possible to substitute apparatus having an equivalent function to the ejector 32 such as a separate pump and mixing chamber. However, such other possible embodiments of the invention would have an increased degree of complexity as well as increased operating costs over the illustrated embodiment. In order to produce a maximum circulation capability, the cryogenic heat exchange system can also be provided with a recirculation heat exchanger 42 to heat the entering liquid cryogen by heat exchange with the portion of the cryogenic heat transfer fluid being recirculated. Since no heat is being transferred outside the system, the total cooling capacity of the cryogen is conserved. The recirculation heat exchanger 42 has first and second passes 44 and 46. The first pass 44 is connected to the high pressure inlet 34 and the second pass 46 is in communication between the low pressure inlet 36 and the outlet 20 of the reversing circuit 16. In the illustrated embodiment, the first and second passes 44 and 46 extend in the same direction but preferably can be set up in a countercurrent flow relationship to transfer a maximum heat from the portion of recirculated cryogenic heat transfer fluid and the entering liquid nitrogen. This heat transfer increases the enthalpy of the liquid nitrogen which increases its motive capacity and thereby increases the rate of recirculated flow within the cryogenic heat exchange system. The degree of circulation and therefore a further control of the temperature of the cryogenic heat transfer fluid can be provided by a proportional valve 48. The condenser 12, the reversing circuit 16, the ejector 32, associated piping, etc. are all generic to a discussion of any cryogenic heat exchange system in accordance with the invention. Any cryogenic heat exchange system of the present invention could have the same layout as the foregoing elements but used in applications other than freeze drying. For instance, a heat exchanger having one or more passes could be connected to a reversing circuit 16 and an ejector such as the ejector 30 to cool foodstuffs passing through one or more cooling ducts. A pressure relief valve 30 and a recirculation heat exchanger 42 could optionally be provided.

Claims: A cryogenic heat exchange system comprising: a heat exchanger having at least one pass for receiving a cryogenic heat exchange fluid; a reversing circuit connected to the at least one pass having an inlet for receiving the cryogenic heat exchange fluid, means for introducing the cryogenic heat transfer fluid into the at least one pass and for reversing flow direction of the cryogenic heat transfer fluid so that the cryogenic heat exchange fluid flows through the at least one pass in one flow direction and then in an opposite flow direction, and an outlet for receiving a portion of the cryogenic heat transfer fluid from the at least one pass after having passed therethrough as spent cryogenic heat exchange fluid; recirculation means connected to the outlet of the reversing circuit for receiving the spent cryogenic heat transfer fluid and having a mixing chamber for mixing the spent cryogenic heat transfer fluid with a cryogen, to form the cryogenic heat exchange fluid and thereby to increase the enthalpy of the cryogenic heat transfer fluid over that of the cryogen, a mixing chamber outlet in communication with the inlet to the reversing circuit for introducing the cryogenic heat transfer fluid into the reversing circuit, and means for circulating the cryogenic heat transfer fluid to the reversing circuit, through the at least one pass and back to the mixing chamber as the spent cryogenic heat exchange fluid; and vent means for venting a remaining portion of the cryogenic heat transfer fluid after having passed through the at least one pass of the at least one heat exchanger. A heat exchanger according to Claim 1 in which the reversing circuit comprises: a pair of first and second valves connecting the at least one pass between the inlet and outlet of the recirculation means such that when the first and second valves are set in an open position, the cryogenic heat transfer fluid flows through the at least one pass in the one flow direction; and a pair of third and fourth valves also connecting the at least one pass between the inlet and outlet of the recirculation means such that when the first and second valves are set in an closed position and the third and fourth valves are set in an open position, the cryogenic heat transfer fluid flows through the at least one pass in the opposite flow direction. A cryogenic heat exchange system according to Claim 1 or Claim 2 in which the recirculation means comprises a venturi-type device having a high pressure inlet for receiving the cryogenic liquid, a low pressure inlet for connection to the outlet of the reversing circuit for drawing the spent cryogenic heat transfer fluid, a low pressure region serving as the mixing chamber and in communication with the high and low pressure inlets, and a high pressure outlet, the high pressure outlet serving as the mixing chamber outlet and connected to the inlet of the reversing circuit for discharging the cryogenic heat transfer fluid into the reversing circuit. A cryogenic heat exchange system according to any preceding claim further comprising a recirculation heat exchanger having a first pass connected to the high pressure inlet of the ejector and a second pass communicating between the outlet of the reversing circuit and the low pressure inlet of the ejector for exchanging heat between the cryogen and the spent cryogenic heat transfer fluid prior to the ejector to increase the enthalpy of the ejector. A freeze dryer comprising: a freezing chamber for subjecting substances to a freeze drying process in which moisture contained within the substances is frozen and sublimated into a vapour; a condenser in communication with the freezing chamber for freezing the vapour and for accumulating the vapour as ice, the condenser having at least one pass for receiving a cryogenic heat transfer fluid for freezing the vapour; a reversing circuit connected to the condenser and having an inlet for receiving the cryogenic heat exchange fluid, means for introducing the cryogenic heat transfer fluid into the at least one pass of the condenser and for reversing flow direction of the cryogenic heat transfer fluid so that the cryogenic heat transfer fluid flows in one flow direction and then in an opposite flow direction, thereby to promote a uniform accumulation of the ice on the condenser, and an outlet for receiving a portion of the cryogenic heat transfer fluid from the condenser as spent cryogenic heat exchange fluid; recirculation means connected to the outlet of the reversing circuit for receiving the spent cryogenic heat transfer fluid and having a mixing chamber for mixing the spent cryogenic heat transfer fluid with a cryogen to form the cryogenic heat transfer fluid and thereby to increase the enthalpy of the cryogenic heat transfer fluid over that of the cryogen, a mixing chamber outlet in communication with the inlet to the reversing circuit for introducing the cryogenic heat transfer fluid into the reversing circuit, and means for circulating the cryogenic heat transfer fluid to the reversing circuit, through the at least one pass of the condenser, and back to the mixing chamber as the spent cryogenic heat exchange fluid; and vent means for venting a remaining portion of the cryogenic heat transfer fluid after having passed through the at least one pass of the condenser. A freeze dryer according to Claim 5 in which the recirculation means comprises an ejector having a high pressure inlet for receiving the cryogenic liquid, a low pressure inlet for connected to the outlet of the reversing circuit for drawing the spent cryogenic heat transfer fluid, a low pressure region serving as the mixing chamber and in communication with the high and low pressure inlets, and a diffuser section in communication with the low pressure region and terminating in a high pressure outlet, the high pressure outlet serving as the mixing chamber outlet and connected to the inlet of the reversing circuit for discharging the cryogenic heat transfer fluid into the reversing circuit. A freeze dryer according to Claim 5 or Claim 6 in which the reversing circuit comprises: a pair of first and second valves connecting the at least one pass between the inlet and outlet of the recirculation means such that when the first and second valve are set in an open position, cryogenic heat transfer fluid flows through the at least one pass in the one flow direction; and a pair of third and fourth valves connecting the at least one pass between the inlet and outlet of the recirculation means such that when the first and second valves are set in a closed position and the third and fourth valves are set in an open position, the cryogenic heat transfer fluid flows through the at least one pass in the opposite flow direction. A freeze dryer according to any one of Claims 5 to 7 in which the recirculation means comprises a venturi-type device having a high pressure inlet for receiving the cryogenic liquid, a low pressure inlet for connected to the outlet of the reversing circuit for drawing the spent cryogenic heat transfer fluid, a low pressure region serving as the mixing chamber and in communication with the high and low pressure inlets, and a high pressure outlet, the high pressure outlet serving as the mixing chamber outlet and connected to the inlet of the reversing circuit for discharging the cryogenic heat transfer fluid into the reversing circuit. A freeze dryer according to any one of Claims 5 to 8, further comprising a recirculation heat exchanger having a first pass connected to the high pressure inlet of the ejector and a second pass communicating between the outlet of the reversing circuit and the low pressure inlet of the ejector for exchanging heat between the cryogen and the spent cryogenic heat transfer fluid prior to the ejector to increase the enthalpy of the ejector.

Inventors: LEE RON CLARK, LEE, RON CLARK
Applicants: BOC GROUP INC, THE BOC GROUP, INC.
Application year: 1994
Main classification: F25D3
IPC codes: F25D3, F26B5